Renewable energy microgeneration system

ABSTRACT

A renewable energy microgeneration system is disclosed. The system comprises one or more portable containers that include a plurality of small holding tanks that are configured to perform at least one of pasteurization and thermophilic anaerobic digestion on waste, a large holding tank that is configured to perform mesophilic anaerobic digestion on the waste after at least one of pasteurization and thermophilic anaerobic digestion is performed, and a de-watering unit that is configured to dry what remains of the waste after mesophilic anaerobic digestion is performed. The system further comprises a controller for automatically moving the waste between the plurality of small holding tanks, the large holding tank, and the de-watering unit as required to facilitate mesophilic anaerobic digestion in the large holding tank. Further, the portable containers are configured to be transported to a site and placed in fluid communication with each other at the site.

CROSS-REFERENCE TO RELATED APPLICATIONS

This application claims priority to U.S. application Ser. No.13/085,320, filed Apr. 12, 2011, which claims the benefit of U.S.Provisional Application No. 61/348,689, filed May 26, 2010, and U.S.Provisional Application No. 61/323,186, filed Apr. 12, 2010, thedisclosures of which are hereby incorporated by reference as if setforth fully herein.

FIELD OF THE INVENTION

The present invention relates to an improved method and device forproviding renewable energy and making users less dependent on localutility providers by recycling their organic waste onsite. Moreparticularly, the present invention relates to improvements to ananaerobic digester that allows users to convert organic waste intosustainable energy.

BACKGROUND OF THE INVENTION

There is a need in the art for a renewable energy microgeneration systemin a single, modular, portable configuration that will allow users toconvert organic waste into sustainable energy onsite. There is also aneed in the art for a renewable energy microgeneration system with areduced footprint, with separate containers for its differentcomponents, with modular interconnectivity between those containers, andwith increased throughput.

SUMMARY OF THE INVENTION

To address at least the problems and/or disadvantages described above,it is a non-limiting object of the present invention to provide arenewable energy microgeneration system. The renewable energymicrogeneration system includes a portable processing container with amixing tank for mixing waste with a liquid, a macerating pump in fluidcommunication with the mixing tank that is configured to macerate thewaste into smaller pieces, a plurality of small holding tanks in fluidcommunication with the mixing tank that are configured to perform atleast one of a pasteurization thermophilic anaerobic digestion on thewaste, a large holding tank in fluid communication with the plurality ofsmall holding tanks that is configured to perform mesophilic anaerobicdigestion on the waste after at least one of a pasteurizationthermophilic anaerobic digestion is performed on the waste, and ade-watering unit in fluid communication with the large holding tank thatis configured to dry what remains of the waste after mesophilicanaerobic digestion is performed on the waste; a controller forautomating the flow of the waste between the mixing tank, the pluralityof small holding tanks, the large holding tank, and the de-watering unitsuch that a user does not need to complete any tasks for performingmesophilic anaerobic digestion after the waste is loaded into the mixingtank; and a portable gas storage container comprising a gas storage tankthat is configured to store biogas generated by the mesophilic anaerobicdigestion, wherein the portable processing container and the portablegas storage container are configured to be transported to a site andplaced in fluid communication with each other so the gas storage tankcan store biogas generated by mesophilic anaerobic digestion in theprocessing container at the site. Those and other objects, advantages,and features of the present invention will become more readily apparentby the following written description, taken in conjunction with theaccompanying drawings and claims.

BRIEF DESCRIPTION OF THE DRAWINGS

Aspects of the present invention can be better understood with referenceto the following drawings, which are part of the specification andrepresent preferred embodiments of the present invention:

FIG. 1A is an isometric view that illustrates an example of an apparatusfor renewable energy microgeneration according to a non-limitingembodiment of the present invention;

FIG. 1B is an isometric view that illustrates the apparatus of FIG. 1Awith the containers and compressor enclosure removed;

FIG. 1C is a plan view that illustrates the apparatus of FIG. 1B;

FIG. 1D is an elevation view that illustrates the apparatus of FIG. 1C;

FIG. 1E is a schematic diagram of the apparatus of FIGS. 1 A-1 CD

FIG. 2 is an isometric view that illustrates a chopper unit according toa non-limiting embodiment of the present invention;

FIG. 3 is an isometric view that illustrates a de-watering unitaccording to a non-limiting embodiment of the present invention;

FIG. 4 is schematic diagram that illustrates a controller according to anon-limiting embodiment of the present invention;

FIG. 5 is an isometric cutaway view that illustrates a gas storage tankaccording to a non-limiting embodiment of the present invention;

FIG. 6 is schematic diagram that illustrates water and waste pipingaccording to a non-limiting embodiment of the present invention;

FIG. 7 is schematic diagram that illustrates gas piping according to anon-limiting embodiment of the present invention; and

FIG. 8 is schematic diagram that illustrates a 6-ton per dayconfiguration of the present invention.

The components in the drawings are not necessarily to scale, emphasisinstead being placed upon illustrating the principles of the presentinvention.

DETAILED DESCRIPTION OF THE INVENTION

The present invention overcomes the shortcomings of the prior artdiscussed above and offers at least the advantages discussed below byproviding a renewable energy microgeneration system in a single,modular, portable configuration that allows users to convert organicwaste into sustainable energy onsite. Moreover, it provides a portablerenewable energy microgeneration system with a reduced footprint, withmodular components and component groupings, and with increasedthroughput. Accordingly, it can be sized to suit a specific user's needsand can be installed and connected to conventional power systems sothat, within a matter of weeks (or hours if the system pre-seeded withlive digestate), a user can create his or her own energy for heating,hot water, and/or general electricity needs.

In more detail, the components of the renewable energy microgenerationsystem work together to perform an anaerobic digestion process thatgenerates heat, electricity, biogas, and fertilizers from what wouldotherwise be considered “waste.” Through its unique configuration, thepresent invention is able to provide all of the components needed tocomplete that process in one or more self-contained shipping containers,thereby providing a portable system that can be conveniently connectedto a wide variety of structures (e.g., homes, industrial buildings, andoutdoor facilities). Moreover, its mobility makes it practical for awide variety of applications, such as providing power in remotevillages, at remote cellular towers, and in war zones or disaster reliefareas where waste is plentiful and power and/or heat are in high demand.

In addition to providing power and heat, the renewable energymicrogeneration system of the present invention also provides a “green”solution to waste management, maximizing the amount of useful energythat can be harnessed from organic materials. It effectively eliminatesthe costs of waste removal by providing the user with a close,convenient place to dispose of his or her waste. It also helps eliminaterunoff pollution. And, in addition to allowing the user to recycle hisor her organic waste onsite, the renewable energy microgeneration systemof the present invention also reduces pollution by making the user lessdependent on utility companies that generate pollution with theirvarious methods of energy production. Moreover, it reduces carbonemissions from waste transport to a centralized processing facility,such as a dump or a larger-scale anaerobic digestion system.

Those and other advantages provided by the present invention can bebetter understood from the description of the preferred embodimentsbelow and in the accompanying drawings. In describing the preferredembodiments, specific terminology is resorted to for the sake ofclarity. However, the present invention is not intended to be limited tothe specific terminology so selected, and it is to be understood thateach specific term includes all technical equivalents that operate in asimilar manner to accomplish a similar purpose.

A. Apparatus for Renewable Energy Microgeneration

Turning to the drawings, FIGS. 1A-1D provide various views of anexemplary apparatus for renewable energy microgeneration 100(hereinafter “the REM apparatus 100”) according to a non-limitingembodiment of the present invention, and FIG. 1E provides a schematicdiagram of the REM apparatus 100 according to a non-limiting embodimentof the present invention. That REM apparatus 100 includes a firstcontainer 102 and a second container 104 that provide portableenclosures that house the various components 106-128 of the REMapparatus 100. The first container 102 houses a chopper unit 106, abuffer tank 108, two small holding tanks 110, a large holding tank 112,a de-watering unit 114, a gas scrubber 116, and an electronic controlunit (ECU) 118. And the second container 104 houses a gas storage tank120. The REM apparatus 100 also includes biogas engine 122 disposedadjacent to the second container 104; a flare 124 disposed on theoutside of the first container 102; a liquor tank 126 disposed adjacentto the first container 102; a compressor 128 disposed in a compressorenclosure 130 adjacent to the first container 102; and various pumps132A-132D, valves 134A-134C, piping 136A-136C, and wiring connections138 for functionally tying those components 106-128 together. Thecomponents 106-128 provided in, on, and adjacent to those containers 102and 104 work together to perform an anaerobic digestion process thatgenerates heat, electricity, biogas, and fertilizers from waste/muck ina mobile, modular renewable energy microgeneration system.

The chopper unit 106 is where muck/waste deposits are loaded into theREM apparatus 100 and it functions to mix that the muck/waste loadedinto the REM apparatus 100 and to mix it with liquid (e.g., potableand/or grey water). The buffer tank 108 functions to store and pre-warmthe water/muck/waste mixture produced with the chopper unit 106. Thesmall holding tanks 110 function to pasteurize the pre-heatedwater/muck/waste mixture produced with the buffer tank 108 or, whenpasteurization is not required for the overall anaerobic digestionprocess, to partially digest that pre-heated water/muck/waste mixturevia thermophilic anaerobic digestion. The large holding tank 112functions to produce mesophilic anaerobic digestion with the partiallypasteurized or digested water/muck/waste mixture produced with smallholding tanks 110. The de-watering unit 114 functions to remove liquidsfrom what remains of the water/muck/waste after anaerobic digestion iscompleted in the small holding tanks 110 and/or the large holding tank112. The gas scrubber 116 functions to clean the biogas produced duringthermophilic and/or mesophilic anaerobic digestion in the small holdingtanks 110 and/or the large holding tank 112, respectively. The gasstorage tank 120 functions to store the cleaned biogas produced with thegas scrubber 116. The biogas engine 122 functions to simultaneouslygenerate electricity and heat from the cleaned biogas stored in the gasstorage tank 120. The ECU 118 functions to control the flow of liquid,muck/waste, water/muck/waste, and biogas through the REM apparatus 100as required to generate heat, electricity, biogas, and fertilizers in acontinuous, regenerative cycle. The flare 124 functions to safely burnsurplus biogas. And the compressor 128 functions to generate compressedair for stirring the water/muck/waste mixture in the small holding tanks110. The containers 102 and 104 and each of those components 106-128 areaddressed separately below.

i. Containers 102 and 104

To enable the REM apparatus 100 to be transported as modular units tosubstantially any location, the containers 102 and 104 that house thevarious components 106-128 of the REM apparatus 100 are configured tocomply with the size and weight requirements of the relevant highwayregulatory and governmental agencies. In FIG. 1A, for example, the firstcontainer 102 (shown with top removed) is a standard 40-foot “High Cube”shipping container (40 ft×8 ft×9.5 ft; Payload: 60,350 lbs; Capacity:2,376 ft³) and the second container 104 (also shown with top removed) isa standard 20-foot shipping container (Dimensions: 19.8 ft×8 ft×8.5 ft;Payload: 48,600 lbs; Capacity: 1,164 ft³). Such containers arespecifically designed to be handled by ship-to-shore gantry cranes, tobe stacked and stored on a container ship, and to be attached to acontainer transport trailer, thereby making those containers 102 and 104particularly suited for commercial land and sea transport. Thosecontainers 102 and 104 are also particularly suited for military airtransport using certain military aircraft, such as Sikorsky SKYCRANEbrand helicopter and the Lockheed C-130 HERCULES brand airplane. Otherstandard containers may also be used (e.g., 45-foot and 30-footcontainers)

a. Base

The first container 102 includes a concrete base that houses some of thepiping 136A-136C that interconnects the components 106-128 of the REMapparatus 100. In manufacture, that piping 136B and 136C is assembledusing a jig to ensure that all the components 106-114 can be positionedcorrectly in a repeatable, modular manner. The jig is manufactured usingan inverse profile of those components 106-114. A straw-based concreteis preferably used to form the base of the container 102 because it is asustainable material that provides a certain degree of flexibilitywithin the concrete base.

The concrete base is designed to support the various components 106-114in the first container 102 by following the profile of the tank bases.That configuration not only provides stability along with the exteriorwalls that hold the tanks in place, it also braces those components106-114 so as to ensure the pipe fittings will not shear in transport.Those components 106-114 may be further braced within the container 102with insulation designed to fit tightly between those specificcomponents 106-114 and the container 102. In the alternative, the baseof the first container 102 may include a metal framework to createstrength and allow for glide entry of the components 106-114 into thefirst container 102.

b. Facia 140 and Loading Platform 142

The first container 102 also includes facia 140 and a loading platform142 at one end of for use in loading muck/waste into the chopper unit106 and for unloading fertilizer output by the de-watering unit 114. Thefacia 140 includes a door 144 that can be opened to allow users accessto the various components 106-114 housed therein. The first container102 also includes a pair of external double doors 146 at the same end ofthe first container 102 as the facia 140. Although those doors 144 arenot shown on the first container 102 for purposes of clarity, they areclearly shown on the second container 104. Those doors 146 are of thetype typically found on a conventional 40-foot or 20-foot shippingcontainer.

The facia 140 provides protection to the user from the components106-114 housed in the first container 102. And the door 144 providesaccess for maintenance and safety checks to be performed on thosecomponents 106-114. The facia 140 may also include access panels (notshown) for accessing parts on the far sides of the components 106 and114 that are disposed adjacent to the facia 140 so as to provide themaximum amount of access and maneuverability to users that need toperform maintenance and/or safety checks on those components 106 and114.

The loading platform 142 is configured allow muck/waste to be loadedinto the chopper unit 106 and to allow solid waste (e.g., mulch) to betransported away from the de-watering unit 114 using a wheelbarrow orother comparable wheeled transport device. The loading platform 142 isalso configured to fold up between the facia 140 and the pair of doubledoors 146 so it can be stowed away during transport of the firstcontainer 102. A control box 148 for operating and monitoring the REMapparatus 100 via the functionality of the ECU 118 is also provided onthe facia 140 and will be folded up behind the double doors 146 of thesecond container 102 during transport. Emergency stop and full shut offsare also located on the facia 140. Because there should not be a need toaccess the gas storage tank 120 after the REM apparatus is placed intooperation (other than routine maintenance and safety checks) thatcomponent 120 preferably remains secured behind the double doors 146 ofthe second container 104 during transport and during operation of theREM apparatus 100.

The loading platform 142 is strong enough to support significantly moreweight than that of the user so large amounts of muck/waste can beloaded into the anaerobic digester at one time. A ramp 150 is also beprovided with the loading platform 142 to allow wheeled transportdevices, such a wheelbarrows, to be easily moved to and from the top ofthe loading platform 142. The ramp 150 is constructed from standardsquare tubes, welded together with mesh spot welds on the top, whichprovides a tractable surface for all weather conditions. The ramp 150 isremovably attached to the loading platform 142 using angled hooks thatclip into a corresponding receiver on the loading platform 142, whichallows users, such as horse yards, to remove the ramp 150 and use theirexisting ramps in its place. The loading platform 142 and ramp 150 arepreferably made from galvanized steel to protect them from the elementsand to reduce manufacturing costs. And the legs of the platform 142 andramp 150 are preferably adjustable according to different terrain toprovide maximum stability, such as on uneven surfaces.

c. Ventilation

A forced ventilation system is preferably incorporated into eachcontainer 102 and 104 to prevent build up of an odorous and explosiveatmosphere. That forced ventilation system includes an electric fan (notshown) that generates a pressure differential between the inside of eachcontainer 102 and 104 and the atmosphere so as to circulate air througheach container 102 and 104 via louvers 152 provided therein. Thatprocess not only prevents dangerous gases from building up in thecontainers 102 and 104, it also removes heat to help cool the machinerylocated in the first container 102. A roof circular vent (not shown) mayalso be provided to allow heat to escape while preventing the ingress ofwater. If the electric fan fails, the ECU 118 will produce an alarm andinitiate shutdown of the various components 106-128 of the REM apparatus100.

d. Roof

The first container 102 and second container 104 may include radiatorroofs that use flexible water piping 136A to heat water using the sun'senergy. Because such standard containers have grooves formed in theirroofs, the flexible water piping 136A can be laid out in those grooves.That water piping 136A will be is covered with a UV-protected plasticsheet to encapsulate heat and, in turn, heat the water within thatpiping 136A. Solar panels may also be placed on the roofs of the firstcontainer 102 and the second container to heat water and/or generateelectricity using the sun's energy. That warm water and electricity canbe used to support the operation of the other components 106-128 of theREM apparatus 100 (e.g., heating muck/waste and/or powering pumps132A-132D and other electronics) and/or it can be used to supplement theheat and electricity generated with the biogas engine 122. Rain watermay also be harvested from the roofs of the containers 102 and 104 foruse in the chopper unit 106. The roofs may also include a lightning rod,or equivalent device, for protecting the containers 102 and 104 andtheir contents from lightning strikes.

ii. Chopper Unit 106

The chopper unit 106 is disposed at a distal end of the first container102 and functions as the input facility for loading muck/waste depositsinto the REM apparatus 100. As FIG. 2 illustrates, the chopper unit 106includes a hopper 200, a mixing tank 202, and a homogenizing pump 204.The hopper 200 is formed as the opening of the chopper unit 106 tofacilitate easier loading of muck/waste therein. The hopper 200 includesa pair of doors 206 that must be opened to load the chopper unit 102.Those doors 206 are accessible at the facia 140 of the first container102 and are held closed with magnetic catches. The hopper 200 ispreferably made from stainless steel or other corrosion resistantmaterial (e.g., galvanized steel) because it is likely to be hit andscratched by shovels/spades or other loading equipment, and the doors206 are preferably made of a durable transparent material (e.g.,plexiglas) so a user can view the mixing/macerating process when thedoors 206 are closed. Those doors 206 also provide a safety feature bypreventing operation of the chopper unit 106 when they are opened,thereby preventing a user or a tool from being pulled into the mixingtank 202 by the homogenizing pump 204. That functionality is controlledby the ECU 118.

The chopper unit 106 also functions to homogenize the muck/waste that ismoved into the mixing tank 202 via the hopper 200. Liquid (e.g., potableand/or grey water) is fed into the chopper unit 106 via water piping136A and mixed with the muck/waste in the mixing tank 202 using thehomogenizing pump 204 to re-circulate, macerate, and homogenize theliquid and muck/waste. The water/muck/waste mixture is chopped finelyenough by the homogenizing pump 204 that it will not clog the wastevalves 134B or the waste piping 136B of the REM apparatus 100 as itmoves between the components 106-114 thereof. Liquid is pumped into themixing tank 202 by a mixer feed pump 132A as required to provide theproper mixture of liquid and muck/waste in the mixing tank 132 requiredfor hydrolysis. That flow rate is controlled by the ECU 118 based on theamount of muck/waste deposited in the mixing tank 202. And the liquid ispreferably grey water that is re-circulated from the de-watering unit114 back into the mixing tank 202 in a regenerative manner to furtheradd to the efficiency of the REM apparatus 100.

The mixing tank 202 is positioned below with hopper 200 so muck/waste isfed directly into the mixing tank 202 via the hopper 200. The mixingtank 132 preferably includes an integrated stone trap 154 (FIG. 1E) tocatch larger debris that that might clog the waste valves 136B or thewaste piping 128B. The stone trap 154 will need to be discharged onregular basis determined after commissioning of the REM apparatus 100and is therefore preferably accessibly via a access hatch in the facia140. The chopper unit 106 can be sized to meet the output requirementsof the user and/or the particular type(s) of muck/waste being processed.And because muck/waste types generally have high volume and low weightor high weight and low volume, the mixing tank 202 will have a visiblelevel marker to which the mixing tank 202 can be filled withsubstantially any type of muck/waste without exceeding the limits of theREM apparatus 100.

The volume indicated by that level marker (e.g., 60 Liters) includesboth the muck/waste loaded into the mixing tank 202 by the user and theliquid fed into the chopper unit 106 via the water piping 136A. The ECU118 will automatically determine the appropriate amount of liquid to mixwith the waste/muck based on the weight and type of the waste/muck. Forexample, very dry and/or dense waste/muck (e.g., horse manure) mayrequire a dilution ratio up to 9:1, while wetter and/or less densewaste/muck (e.g., vegetable waste) may require a dilution ration ofaround 4:1. Because the dense waste/muck necessarily weighs less thanthe less dense waste muck, the resulting overall volume ofwater/waste/muck in the mixing tank 108 will be the same regardless ofwhich of those types of waste/muck is placed therein (i.e., 15 kg horsemanure and 45 kg of vegetable waste will both fill a 60 Liter volumewhen the proper amount of liquid is added). The type and/or weight ofthe waste/muck can be input into the ECU 118 by a user and/orautomatically measured by the ECU 118, such as with an electronic scale,so the ECU 118 can determine the appropriate amount of liquid to mixwith that waste/muck.

iii. Buffer Tank 108

The buffer tank 108 receives the water/muck/waste mixture from thechopper unit 106 and stores it before moving it to the small holdingtanks 110. Because it is used for storage rather than just mixing, thebuffer tank 108 is sized larger than the mixing tank 202 of the chopperunit 106. The water/muck/waste mixture is moved from the mixing tank 202of the chopper unit 106 to the buffer tank 108 with the homogenizingpump 204 by opening one waste valve 134B and closing another so as toclose the re-circulation loop and re-redirect the water/muck/wastemixture to the buffer tank 108. The opening and closing of those wastevalves 134B is controlled by the ECU 118 based on predetermined cycletimes.

The buffer tank 108 functions as a “buffer” for the small holding tanks110 and large holding tank 112 by warming the water/muck/waste mixturebefore it is moved into the small holding tanks 110 and large holdingtank 112. That warming is preferably performed by a heat exchanger 156that is disposed in the buffer tank 108. The heat exchanger 156 receivesheat energy by pumping the heated and partially pasteurized or digestedwater/muck/waste produced with the small holding tanks 110 through theheat exchanger 156 before depositing it into the large holding tank 112.That exchange of heat energy is essential not only to complete thepasteurization process when pasteurization is necessary, but also toreduce the temperature of the heated and partially pasteurized ordigested water/muck/waste mixture to 35-40° C. before it is deposited inthe large holding tank 112.

That heated and partially pasteurized or digested water/muck/waste ispumped by a digester feed pump 132B that is controlled by the ECU 118and operates to feed the heated and partially pasteurized or digestedwater/muck/waste into the large holding tank 112. That operation notonly serves to pre-heat the water/muck/waste mixture before moving it tothe small holding tanks 110, it beneficially removes heat from theheated and partially pasteurized or digested water/muck/waste beforemoving it to the large holding tank 112. As discussed below, the heatedand partially pasteurized or digested water/muck/waste is preferablycooled down to about 40° C. before being depositing into the largeholding tank 112.

The waste piping 136B through which the pre-heated water/muck/waste ismoved to the small holding tanks 110 is preferably fitted within thefloor of the container 102 so the buffer tank 108 can be drained fromthe bottom and the small holding tanks 110 can be fed from the bottom.If space does not permit and the small holding tanks 110 must be fedfrom the top, the feed tubes preferably extend to the bottom of thebuffer tank 108 and/or each small holding tank 110 so that the mixturewill be withdrawn from the bottom of the buffer tank 108 and/ordeposited in the bottom of the small holding tanks 110. The buffer tank108 is preferably sized to allow continuous operation of the REMapparatus 100 for at least 2 days. And it is preferably made out ofsteel or fiberglass to reduce manufacturing costs.

iv. Small Holding Tanks 110

Returning to FIGS. 1A-1E, the pre-heated water/muck/waste is pumped fromthe buffer tank 108 to the small holding tanks 110 by a pasteurizationfeed pump 132C. That pump 132C operates on a predefined feeding cyclethat is controlled by the ECU 118. In the small holding tanks 110, thepre-heated water/muck/waste is heated and stirred to producepasteurization or, if pasteurization is not required for the overallanaerobic digestion process, to produce thermophilic anaerobicdigestion. The pre-heated water/muck/waste in each small holding tank110 is continuously stirred with a gas mixer 158 (FIG. 1E) to keep thesolids and liquids in suspension during the pasteurization orthermophilic anaerobic digestion process. That mixture is heated withheaters 160 (FIG. 1E) capable of heating the mixture contained thereinto around 55-75° C. The gas mixers 158 are pressurized with thecompressor 128 and include nozzles that inject air directly into thebottom of each small holding tank 110 to promote aerobic thermophilicdigestion, thereby supplementing the heating requirements duringpasteurization. And the heaters 140 are either electric immersionheaters or water-based boiler-fed coil heaters that are disposed in theinside of the small holding tanks 110 so that the water/muck/wastemixture can be heated directly.

Each of the small holding tanks 110 has a relatively small volume (e.g.,around 1,800 Liters) to reduce the energy required to heat thewater/muck/waste disposed therein. Loads on the heaters 160 can befurther reduced by recovering heat from the biogas engine 122 and/or theengines that drive the homogenizing pump 204, the de-watering unit 114,or any of the other pumps 132A-132D of the REM apparatus 100 in aregenerative manner so as to further increase the efficiency of the REMapparatus 100. And as discussed above, the small holding tanks 110 canbe used to perform either pasteurization or thermophilic anaerobicdigestion on the water/muck/waste disposed therein, depending on whetherpasteurization is required for the overall anaerobic digestion process.If they are used to perform thermophilic anaerobic digestion, biogaswill be generated in the small holding tanks 110 and similar precautionsto those discussed below with respect to the large holding tank 112 willneed to be taken (e.g., mixing the water/muck/waste with biogas insteadof air, drawing off biogas to the gas storage tank, separating the smalldigester tanks 110 from machinery and electronics that may produce aspark, etc.). The small holding tanks 110 may also be used for otherpurposes, such as arresting the digestion process of the grey water inthe liquor tank 126.

The small holding tanks 110 are operated in batch mode that includesoffset cycles of feeding, holding, and discharge. For example, after thefirst small holding tank 110 is fed and filled with pre-heatedwater/muck/waste from the buffer tank 108, it will hold that pre-heatedwater/muck/waste while it is stirred and heated, as discussed above. Thesecond small holding tank 110 will be fed and filled after the firstsmall holding tank 110. The heated and partially pasteurized or digestedwater/muck/waste will then be discharged from first small holding tank110 while the second small holding tank 110 holds, stirs, and heats thepre-heated water/muck/waste with which it was filled. And the heated andpartially pasteurized or digested water/muck/waste will then bedischarged from first second holding tank 110 while the second smallholding tank 110 is filled with a new batch of pre-heatedwater/muck/waste from the buffer tank 108. Water/waste/muck is cycledthrough the small holding tanks 110 in that manner as required isrepeated back and forth between the first and second digested tanks 110.The fill quantities are controlled by the ECU 118 using a set of levelsensors (LS) in the small holding tanks 110. And although only two smallholding tanks 110 are shown in FIGS. 1A-1E, the REM apparatus may use asmany small holding tanks 110 are required to meet a user's processingdemands.

The waste piping 136B through which the heated and partially pasteurizedor digested water/muck/waste is moved to heat exchanger 136 in thebuffer tank 108 is preferably fitted within the floor of the container102 so that mixture can be fed up through the bottom of the buffer tank108 so as to provide the proper temperature gradient (i.e., hottest onthe bottom and coolest on the top) as the heated and partiallypasteurized or digested water/waste/muck flows through the heatexchanger 156 in the buffer tank 108 and toward the large holding tank112. Each small holding tank 110 is insulated to improve its efficiency.Preferably, the small holding tanks 110 are formed from PVC to reducemanufacturing costs and a “green” material, such as sheepswool, is usedto form the insulation. The insulation can be formed in modular,interlocking pieces that can be connected together to surround the smallholding tanks 110.

v. Large Holding Tank 112

The heated and partially pasteurized or digested water/muck/waste ispumped from the small holding tanks 110 to the large tank 112 by thedigester feed pump 132B. Like the pasteurization feed pump 132C, thedigester feed pump 132B operates on a predefined feeding cycle that iscontrolled by the ECU 118. Because the heated and partially pasteurizedor digested water/muck/waste must be cooled to approximately 40° C.before it is deposited in the large holding tank 112, it passes throughthe heat exchanger 156 in the buffer tank 108 as it is pumped from thesmall holding tanks 110 to the large tank 112. The heated and partiallypasteurized or digested water/muck/waste is cooled by passing its heatenergy to the water/muck/waste mixture in the buffer tank 108 via theheat exchanger 156, as discussed above. In that manner, the heat energyexpended to support pasteurization or thermophilic anaerobic digestionin the small holding tanks 110 is re-used in a regenerative manner,thereby further increasing the efficiency of the REM apparatus 100.

In the large holding tank 112, the pasteurized or cooled and partiallydigested water/muck/waste is stirred to produce mesophilic anaerobicdigestion. Like the pre-heated water/muck/waste in each small holdingtank 110, the pasteurized or cooled and partially digestedwater/muck/waste in the large holding tank 112 is continuously stirredwith a gas mixer 158 (FIG. 1E) to keep the solids and liquids insuspension while biogas (e.g., methane and carbon dioxide) accumulatesat the top of the large holding tank 112. However, unlike the pre-heatedwater/muck/waste in each small holding tank 110, which is stirred withcompressed air from the compressor 128, the pasteurized or cooled andpartially digested water/muck/waste in the large holding tank 112 isstirred by re-circulating biogas through the gas mixer 158 using acorrosive gas vacuum pump 162. In the absence of air, bacterialpopulations break down organic solids in the water/muck/waste mixtureinto biogas and more stable solids. Thus, biogas is used to stir thewater/muck/waste instead of air because introducing oxygen into thatmixture would create an explosive atmosphere. In the alternative, amixing pump (not shown) could be used to mix the water/muck/wastemixture by intermittently circulating it within large holding tank 112.

The operating temperature of the large holding tank 112 is preferablybetween 32-40° C. Those lower temperatures allow the large holding tank112 be have a greater volume (e.g., around 14,000 Liters) than the smallholding tanks 110 because less energy is required to maintain thoselower temperatures. In fact, the large holding tank 112 may need to becooled instead of heated. To serve that purpose, the large holding tank112 may be made as a dual layer tank so that cooling fluid (e.g.,potable and/or grey water) can be circulated between the inner and outershells to cool the water/muck/waste disposed in the inner shell. The useof a conductive material, such as steel, on the inside shell and aninsulating material on the outside shell provide a suitable way ofachieving that functionality.

In the alternative, the large holding tank 112 may be formed as a singletank using low cost fiber reinforced thermoforms. That material allows aplurality of large holding tanks 112 to be rapidly manufactured usinginexpensive molds. That material is also flexible so the large holdingtanks 112 will not break if dropped when full of liquid (e.g., 1.5meters full moving at 20 kph). In either embodiment, the large holdingtank 112 may be painted with conditioned nanotech carbon in the shape ofa lotus leaf to repel bacteria and with silicates to prevent methanefrom tunneling/leaking through tank walls. The large holding tank 112 ispreferably immune to two types of bacteria—anammox bacteria andmethagenic bacteria, which are used to eat both ammonia and to breakdown carbon chains. The large holding tank 112 may also include acathode and anode that harvest free electrons from the digestion processso that the large holding tank 112 can be used as a big battery forpowering the REM apparatus 100 or for providing power to otherapparatus. The small holding tanks 110 may be similarly constructed.

The large holding tank 112 operates on a “draw and fill” mode where aknown quantity of water/muck/waste is drawn into the large holding tank112 by the digester feed pump 132C until it is filled to apre-determined level. The draw and fill quantities are controlled by theECU 118 using a set of level sensors (LS) in the large holding tank 112.The feed flowrate of water/muck/waste to the large holding tank 112 iscontrolled by the ECU 118 such that it provides a minimum retention timeof 15 days for the mesophilic anaerobic digestion process. And duringthe draw down process, biogas is preferably drawn back into the largeholding tank 112 from the gas storage tank 120 to maintain an operatingpressure of 15-20 mbar within the large holding tank 112.

The large holding tank 112 is sufficiently sealed to prevent gaseousoxygen from entering the system and hindering the anaerobic digestionprocess. The large holding tank 112 includes a safety relief valve 164that vents outside of the first container 102 and releases pressure fromthe large holding tank 112 if that pressure approaches unsafe levels.The large holding tank 112 is also insulated to improve its efficiency.Preferably, the outside shell of the large holding tank 112 is formed offiberglass to reduce manufacturing costs and a “green” material, such assheepswool, is used to form the insulation. The insulation can be formedin modular, interlocking pieces that can be connected together tosurround the large holding tank 112.

As mesophilic anaerobic digestion is performed in the large holding tank112, biogas collects at the top of the large holding tank 112. Althoughthe pneumatic pump re-circulates some of that biogas back into thewater/muck/waste as part of the mixing operation, the remainder of thebiogas is drawn from the large holding tank 112 and pumped through thegas scrubber 116 before being deposited in the gas storage tank 120.That biogas is preferably discharged from the large holding tank 112 atan operating pressure of 15-20 mbar. And after the mesophilic anaerobicdigestion process is completed, the digested water/muck/waste mixture ispumped to the de-watering unit 114 by a sludge draw-off pump 132D thatis controlled by the ECU 118 based on the retention time required forthe mesophilic anaerobic digestion process.

Because methane and other combustible gases are generated in the largeholding tank 112, it may be necessary to provide it in a separatecontainer from some of the other components of the REM apparatus 100—inparticular, those components that contain moving machinery andelectronics that may generate a spark (e.g., the chopper unit 106, thede-watering unit 114, the biogas engine 122, the air compressor 128, themixer feed pump 132A, the digester feed pump 132B, the pasteurizationfeed pump 132C, the sludge draw-off pump 132D, the gas vacuum pump 162,and the homogenizing pump 204). In the alternative, a container can bedivided into separate spaces using air-tight bulkheads to separate thelarge holding tank 112 from the machinery and electronics of the REMapparatus 100. Such a separate container or container space willpreferably provide full hazardous material and explosive atmosphereseparation from the machinery and electronics of the REM apparatus 100in accordance with local, national, and/or international standards, suchas the European Union's Atmospheres Explosibles (ATEX) directive andDangerous Substances and Explosive Atmospheres Regulations (DSEARs).

vi. De-Watering Unit 114 and Liquor Tank 126

The de-watering unit 114 removes liquids from the fully digestedwater/muck/waste to produce a compost bi-product and thickened digestatethat can be used as solid and liquid fertilizers. As FIG. 3 illustrates,the de-watering unit 114 includes a de-watering tank 300 where thedigested water/muck/waste is received from the large holding tank 112.The de-watering unit 114 also includes a conveyor tube 302 and anelectric motor 304 for rotating a shaftless screw conveyor disposedwithin the conveyor tube 302. As it rotates, the screw conveyortransports the solid muck/waste from the water/muck/waste mixture inde-watering tank 300 up through the conveyor tube 302 and out through aspout 306 disposed at the upper end of the conveyor tube 302. That solidmuck/waste can be collected in a bin placed below the spout on theloading platform 142 for use as solid fertilizer. And the remaining greywater, or liquor, in the de-watering tank 300 is then gravity fed intothe liquor tank 126 for use as liquid fertilizer.

The de-watering unit 114 is disposed adjacent to the chopper unit 106 atthe same end of the first container 102 so that the process of thepresent invention is completed at the same location it begins.Accordingly, the user can load muck/waste into the chopper unit 106 andextract the resulting solid fertilizer produced via the anaerobicdigestion process at the same location. The liquor tank 126 ispreferably disposed adjacent to the first container 102 at that same endfor the same purpose. And although the anaerobic digestion process maytake a few weeks to complete, after the first cycle is complete, thereshould be solid and liquid fertilizers ready to be extracted each timethe user goes to load the chopper unit 106 with new muck/waste. Thesolid fertilizer may be mulch that is suitable for animal bedding. Andat least a portion of the grey water may be re-circulated with the mixerfeed pump 132A for mixture with muck/waste that is loaded into themixing tank 132 as required for hydrolysis. The re-circulation of thegrey water with the mixer feed pump 132A is controlled by the ECU 118 byautomatically operating that pump 132A and opening/closing theassociated water valves 134A as required direct the flow of the greywater.

The liquor tank 126 is disposed adjacent to the first container 102 at alocation near and below the de-watering tank 300 of the de-watering unit114 so the solid fertilizer and liquid fertilizer produced with thede-watering unit 114 can be gravity fed into the liquor tank 126. Toserve that purpose, the de-watering tank 300 is disposed on a base 308that supports it at a location above the liquor tank 126. The liquortank 116 is preferably made of PVC to reduce manufacturing costs. Andalthough the liquor tank 126 is illustrated as being disposed adjacentto the first container 102, it may also be disposed inside the firstcontainer 102 in a similar relationship to the de-watering unit 114.

vii. Gas Scrubber 116

The gas scrubber 116, or de-sulphurization unit, is disposed between thelarge holding tank 112 and the gas storage tank 120. It is configured toclean the biogas extracted from the water/muck/waste in the largeholding tank 112 before it is stored in the gas storage tank 120. Thegas scrubber 116 may be any suitable type, such as an activated carbonfilter or a compressed gas filter (e.g., an amine gas filter). The gasscrubber 116 is used to treat the biogas and refine it for use asfuel—namely by reducing the levels of hydrogen sulfide in the biogas.However, the gas scrubber 116 may not be needed if the biogas does notneed to be treated, such as when it is not going to be used for fuel ordoes not contain prohibited levels of certain chemicals.

viii. Electronic Control Unit (ECU) 118

The flow of liquid (e.g., potable and/or grey water), muck/waste, andbiogas through the REM apparatus 100 of the present invention iscontrolled by the ECU 118. As FIG. 4 illustrates, the ECU 118 includes aprogrammable logic controller (PLC) that is programmed to monitor,record, and control the various stages of the anaerobic digestionprocess (e.g., temperatures, volumes, and flow rates). It providesvisual feedback of those operations to the user via a graphical userinterface, such as a computer monitor or touchscreen. The ECU 118automates the anaerobic digestion process by turning the variouscomponents 106-128 of the REM apparatus 100 on and off based on thevalues it monitors and records. The ECU 118 makes the determination asto which components 106-128 to turn on and off primarily based on thecontent of the muck/waste loaded into the REM apparatus 100, which canbe detected with the appropriate sensors and/or can be input by a uservia a user interface at the ECU 118.

For example, the ECU 118 will automatically operate the appropriatepumps 132A-132D, 204, and 162 and open/close the appropriate valves134A-134C to pump the fully digested water/muck/waste from the largeholding tank 112 to the de-watering unit 114 after it detects that theanaerobic digestion process is completed. The ECU 118 will automaticallyfeed, hold, and discharge water/muck/waste from the small holding tanks110 in batch mode based on levels detected with level switches (LS) andthe times over which the water/muck/waste has been held in each smallholding tank 110. The ECU 118 will determine whether or not to activatethe heaters 160 in the small holding tanks 110 based on temperaturesensors (TS) in each small holding tank 110. And the ECU 118 willautomatically determine the flow rates and cycle times for moving thewater/muck/waste between the different components 106-128 of the REMapparatus 100 by monitoring the anaerobic digestion process in itsvarious stages using a clocking circuit, level sensors (LS) temperaturesensors (TS), and pressure sensors (PS) located throughout the REMapparatus 100, thereby allowing the ECU 118 to adjust the anaerobicdigestion process in real time as required to maintain optimaldigestion.

The ECU 118 can determine such things as the amount of liquid to add tothe muck/waste mixture and the amount of biogas expected to be producedfrom that muck/waste based on the answers to a series of questionspresented to the user via the graphical user interface of the ECU 118.For example, the user could be asked to input a description of the sitewhere the muck/waste was collected, the availability of services,waste/muck type (e.g., manure, vegetable waste, etc.), waste/muckquantities, the intended use of the mulch that will be produced, and theintended use of the grey water that will be produced. Thus, by allowinga user to input the answers to those questions for different batches ofmuck/waste loaded into the REM apparatus 100, the ECU 118 is able tocustomize the digestion process for each batch of muck/waste loaded intothe REM apparatus 100. Some of those answers may also be obtainedautomatically by the ECU 118, such as using a scale provided on thechopper unit 106 or the loading platform 142 to weigh the muck/wasteloaded into the REM apparatus 100.

The PLC of the ECU 118 is also programmed to monitor and maintain safetythroughout the anaerobic digestion process. That monitoring not onlyallows close control of machinery and electrical equipment to preventphysical injury to users, it also allows close control the processparameters that are used as Hazard Assessment and Critical ControlParameters (HACCPs). For example, the ECU 118 monitors the biogaspressure in the gas storage tank 120 and the levels of water/muck/wastein the small holding tanks 110 and large holding tank 112 to make surethey are maintained at safe operating levels (e.g., a level sensor (LS)will be provided in the small holding tanks 110 and large holding tank112 to ensure that the immersion heaters 160 are not trying to heat anempty tank). Alarms will sound if/when the volumes of biogas and/orvolumes of water/muck/waste approach unsafe levels. The ECU 118 alsoincludes a supervisory control and data acquisition (SCADA) interfaceand/or Internet and wireless (e.g., GSM, GPRS, wife, etc.) functionalityfor providing the user with remote monitoring capabilities forefficiency, diagnostics, operations, and safety. Preferably, the ECU 118is provided at the same end of the first container 102 as the chopperunit 106, de-watering unit 114, and liquor tank 126 so the anaerobicdigestion process can be controlled from the same location thatmuck/waste is loaded into the REM apparatus 100 and fertilizer isremoved from the REM apparatus, thereby providing an added level ofconvenience to the user.

The ECU 118 includes a human-machine interface (HMI) for communicatingwith the various components 106-128, pumps 132A-132D, and valves134A-134C of the REM apparatus 100. It also includes a cloud monitoringapplication for regionally monitoring the status of those components106-128, pumps 132A-132D, and valves 134A-134C128. Communication can beestablished with the ECU 118 via the SCADA interface and/or Internet andwireless functionality using substantially any computing device (e.g.,personal computer, laptop computer, tablet computer, personal digitalassistant (PDA), smart phone, etc.) so as to allow a user to remotelymonitor, control, and troubleshoot the REM apparatus 100. For example,smart phone applications can communicate with the ECU 118 via a businterface to a canbus node that communicates to low cost sensors anddevices, such as those used in the automotive industry.

All of the interfaces for a user to input information into and otherwisecontrol the operation of the ECU 118 are provide in the control box 148located on the facia 140 of the first container 102 so the user canoperate the different components 106-128 of the REM apparatus 100 fromthe same location where muck/waste is loaded into the REM apparatus 100and solid and liquid fertilizers are removed from the REM apparatus 100,thereby adding an additional level of convenience to the user. Thecontrol box 148 and its associated interfaces are in electrical datacommunication with the ECU 118 via electrical wiring 138. Or in thealternative, they may be in wireless data communication with each othervia any suitable, secure wireless functionality (e.g., GSM, GPRS, wifi,etc.).

The ECU 118 also provides a central source of power for the variouscomponents 106-128, pumps 132A-132D, and valves 134A-134C of the REMapparatus 100. It includes a miniature circuit breaker (MCB) for each ofthose components 106-128, pumps 132A-132D, and valves 134A-134C as wellas light emitting diodes (LEDs) that indicate their respective status(e.g., “on”, “fault”, etc.). Those MCBs may are accessible via a breakerbox 166 (FIG. 1A) disposed on the outside of the first container 102.The breaker box 166 is disposed on the outside of the first container102 so that those MCBs can be easily accessed without needing to go intothe container 102 where the risks of user injury are higher due to theamount of machinery housed therein. The other components of the ECU 118are preferably disposed in an enclosure inside the first container 102to provide better protection from the elements.

The power bus of the ECU 118 preferably receives its power from a 16amp, 240 volt mains power supply. It may also receive its power from thebiogas engine 122. And although FIG. 5 only shows four temperaturesensors (TS) and seven “low” level switches (LS), the ECU 118 isconnected to several other temperature sensors (TS) and level sensors(LS) to support its control of the REM apparatus 100. For example, theECU 118 also includes at least seven “high” level sensors (LS) and atleast three additional temperature sensors (TS). See, e.g., FIG. 1E. TheECU 118 may also be connected to other types of sensors, such as gascomposition sensors, pressure sensors (PS), voltmeters, etc., asrequired to support its control of the REM apparatus 100. The wiring 138of the ECU 118 and its various connections are compliant with the local,national, and/or international standards, such as those set forth in theWater Industry Mechanical and Electrical Specification (WIMES).

ix. Gas Storage Tank 120

After the biogas is extracted from the large holding tank 112, and afterit is cleaned by the gas scrubber 116 (when cleaning is required), it isstored in the gas storage tank 120. As FIG. 5 illustrates, the gasstorage tank 120 includes a flexible bladder 500 disposed inside asolid, double-walled tank 502. The double-walled tank 502 may be filledwith liquid (e.g., potable and/or grey water) and constructed of asufficiently strong material to withstand the high pressures associatedwith storing the biogas under pressure. The gas storage tank 120includes a water inlet 504 and a water outlet (not shown) so the liquidcan be pumped into and out of the double-walled tank 502 via waterpiping 136A to equalize and maintain a constant, fixed pressure ofbiogas in the flexible bladder 500. The gas storage tank 120 alsoincludes a safety relief valve 168 that vents outside of the secondcontainer 104 and releases pressure in the flexible bladder 500 if thatpressure approaches unsafe levels. Any surplus biogas that cannot bestored by the gas storage tank 120 is safely burned off with the flare124 so as to prevent unsafe levels of pressure occurring. That flare 124has a pilot light that is powered by a propane tank 170 provided in oradjacent to the first container 102.

To measure the volume of gas stored in the flexible bladder 500, aseparate flow meter is provided at the inlet and outlet gas piping 136Cof the gas storage tank 120. The difference between the readings atthose flow meters is used by the ECU 118 to monitor the amount of gasstored in the gas storage tank 120. Also provided at the outlet gaspiping 136C is a flow control valve 134C for controlling the flow ofbiogas from the gas storage tank 120 and a flame arrestor (not shown)for preventing a flame from propagating back through the flow controlvalve 134C into the gas storage tank 120. In that way, biogas can beextracted from the gas storage tank 120 as needed and used to generateheat, electricity, or any other form of gas-generated energy. One of thedevices that is used to generate heat and electricity is the biogasengine 122.

Because methane and other combustible gases are stored in the gasstorage tank 120, it may be necessary to provide it in a separatecontainer 104 from some of the other components of the REM apparatus100—in particular, those components that contain moving machinery andelectronics that may generate a spark (e.g., the chopper unit 106, thede-watering unit 114, the biogas engine 122, the air compressor 128, themixer feed pump 132A, the digester feed pump 132B, the pasteurizationfeed pump 132C, the sludge draw-off pump 132D, the gas vacuum pump 162,and the homogenizing pump 204). In the alternative, a container can bedivided into separate spaces using air-tight bulkheads to separate thelarge holding tank 112 from the machinery and electronics of the REMapparatus 100. Such a separate container or container space willpreferably provide full hazardous material and explosive atmosphereseparation from the machinery and electronics of the REM apparatus 100in accordance with local, national, and/or international standards, suchas the European Union's ATEX directive and DSEARs.

x. Biogas Engine 122

The outlet gas piping 136C from the gas storage tank 120 is connected tothe biogas engine 122, which simultaneously produces electricity andheat from the biogas via a combustion engine (e.g., an internalcombustion engine or a Stirling engine). The biogas engine 122 ispreferably a 3,600 kWh combined heat and power (CHP) unit. The CHP unitcan be a modified diesel genset that bums biogas or a pyrolsis-basedsyngas/biogas burning steam engine (e.g., a sterling format or rotarypiston engine that drives a generator directly).

Because the biogas engine 122 requires a specific input pressure tooperate (e.g., 100 mbar), biogas is maintained in the gas storage tank120 at that pressure using a booster fan 172. The electricity producedwith the biogas engine 122 can be linked to the user's power grid andused to power household devices, such as lights and appliances. And theheat produced can be linked to the user's heating, ventilation, and airconditioning (HVAC) system and/or water heating system and used forspace heating and/or water heating. The biogas engine 122 may also beused to power the various pumps 134A-134D, 204, and 162 of the REMapparatus, or any component 106-128 that runs on electricity, and toprovide heat to the small holding tanks 110 to further improve theefficiency of the present invention.

To further the mobility of the REM apparatus 100, the biogas engine 122is preferably provided on its own trailer. It is also preferablyconnected to the gas storage tank 120, the power bus of the ECU 118, anda user's power grid using standard connections.

xi. Flare 124

The flare 124 produces flame that burns surplus methane and/or propaneto the European Union's particulate standard. The flare 124 includes apilot light that is connected to the propane tank 170 via gas piping134B to ensure that surplus biogas is instantly lit and remains lit soit does not gather in unsafe, combustible amounts in and/or around theREM apparatus 100. The flare may include two separate pilot lights—afirst pilot light that burns methane and a second pilot light that burnspropane. A piezoelectric lighter or an auto ignition system with visualflame detection may also be used and integrated with the functionalityof the ECU 118 for automated triggering.

xii. Piping 136A-136C

a. Water Piping 136A

The water piping 136A may be any suitable low-pressure piping, such asPVC piping, for feeding liquid (e.g., potable and/or grey water) intothe chopper unit 106. As FIG. 6 illustrates, the water piping 136Adelivers potable water to the chopper unit 106 from an outside watersource, such as a well or a local utility, and delivers grey water tothe chopper unit 106 from the de-watering unit 114. To allow the REMapparatus 100 to be connected to an outside water source, the waterpiping 136A preferably includes a standard connector, such as a gardenhose connector, at an inlet location on the outside of the firstcontainer 102.

As FIG. 6 also illustrates, the grey water from the de-watering unit 114is circulated between the inner shell and outer shell of the largeholding tank 112 and between the outer shell and the bladder of the gasstorage tank 120 to aid in the cooling of the contents of the largeholding tank 112 and the gas storage tank 120. The ECU 118 controls theamount of cooling provided as required to maintain the desired operatingtemperatures in the large holding tank 112 and the gas storage tank 120by opening and closing the appropriate water valves 134A and operatingthe mixer feed pump 132A. And although FIG. 6 shows grey water beingpumped through both the large holding tank 112 and the gas storage tank120, one or both of those components 112 and 120 can be bypassed byopening and closing the appropriate water valves 134A.

b. Waste Piping I36B

The waste piping 136B provides a complex network that works its wayaround the fixed components 106-128 of the REM apparatus 100. Standardpipe lengths are used where possible to facilitate ease ofmanufacturing. The material used for the waste piping 136B is preferablyHDPE. The properties of that material allow it to withstand chemical andbiological attack, to withstand temperatures up to 137° C., and towithstand pressures up to 12 bar. Moreover, its insulating propertieshelp further improve the efficiency of the REM apparatus 100. A standarddrain connection is preferably provided on the outside of the firstcontainer 102 to facilitate connecting the waste piping 136B to a sumpfor draining the buffer tank 108, small holding tanks 110, large holdingtank 112, liquor tank 126, mixing tank 202, and de-watering tank 300 asrequired to clean and maintain them.

As FIG. 6 also illustrates, the waste piping 136B delivers thewater/muck/waste mixture to the buffer tank 108 before delivering it tothe small holding tanks 110. Then, the heated and partially pasteurizedor digested water/muck/waste mixture passes through the heat exchanger156 in the buffer tank 108 as it is moved from the small digesters tanks110 to the large holding tank 112. And after mesophilic anaerobicdigestion is completed in the large holding tank 112, the fully digestedwater/muck/waste mixture is moved to the de-watering unit 114. The ECU118 controls the amounts water/muck/waste moved between those components106-114 as required to optimize the anaerobic digestion process byopening and closing the appropriate waste valves 134E and operating thedigester feed pump 132B, the pasteurization feed pump 132C, the sludgedraw-off pump 132D, and the homogenizing pump 204. And although FIG. 6shows the heated and partially pasteurized or digested water/muck/wastemixture being pumped through the heat exchanger 156 in the buffer tank108, the heat exchanger 156 can be bypassed by opening and closing theappropriate waste valves 134B.

c. Gas Piping 136C

The gas piping 136C is preferably stainless steel due to the corrosiveproperties of elements within biogas. For example, there may be H₂S(Hydrogen Sulphide) in the biogas. Stainless steel piping does not reactwith that medium. And as FIG. 7 illustrates, the gas piping 136C formstwo separate loops. The first loop circulates air through the smallholding tanks 110 with the compressor 128 to stir the water/muck/wastein the small holding tanks 110. And the second loop circulates biogasthrough the large holding tank 112 with the gas vacuum pump 162 to stirthe water/muck/waste in the large holding tank 112. The first loop is an“open” loop because it allows the introduction of air into the smallholding tanks 110, and the second loop is a “closed” loop because itonly utilizes the biogas already in the large holding tank 112.

The second loop also moves biogas from the large holding tank 112 to thegas storage tank 120 after scrubbing it with the gas scrubber 116. Fromthe gas storage tank 120, the scrubbed biogas is moved to the biogasengine 122 using a booster fan 172 to maintain the biogas at theoperating pressure required for the biogas engine 122. Any surplusbiogas that cannot be stored by the gas storage tank 120 is safelyburned off with the flare 124 so as to prevent unsafe levels of pressureoccurring. And as discussed above, biogas may be circulated back intothe large holding tank 112 to maintain the desired operating pressuretherein during the draw down process. The ECU 118 controls the amountsof biogas moved between those components 112, 116, 120, and 122 asrequired to perform those operations by opening and closing theappropriate gas valves 134C and operating the gas vacuum pump 162 andthe booster fan 172. And although FIG. 7 shows biogas being circulatedback into the large holding tank through the gas scrubber 116, the gasscrubber 116 can be bypassed to perform that operation by opening andclosing the appropriate gas valves 134C while the gas vacuum pump 162 isrun in reverse. And although FIG. 7 shows two separate loops, thoseloops may be interconnected as required to recover biogas from the smallholding tanks 110.

xiii. Exhaust Stacks 174

To contend with the potentially bothersome odors generated by theanaerobic digestion process, the buffer tank 108, small holding tanks110, de-watering unit 114, and liquor tank 126 are each provided with anexhaust stack 174 with a filter element. The filter element preferablyutilizes organic filtering material, such as a combination of steel wooland ferns, to remove potentially bothersome odors from the gasesgenerated in those components 108, 110, 114, and 126. And the exhauststacks 174 preferably extend through the roof of the first container 102so as to vent those gases outside of the first container 102. Asdiscussed above, the large holding tank 112 does not include an exhauststack 174 because the biogas generated therein is highly combustible.Accordingly, that biogas is either stored in the gas storage tank 120 orburned off by the flare 124.

B. Method for Renewable Energy Microgeneration

The components 106-128 of the REM apparatus 100 are best described asforming separate nodes in the anaerobic digestion process. At node 1,the chopper unit 106 receives muck/waste (e.g., feedstocks) of variablesolids contents that have to be diluted down to about 8-10% total solidsand a ratio of about 1:4 of waste/muck to dilution liquid (e.g., potableor grey water). Dilution is achieved by adding the recycled grey waterrecovered from the fully digested water/muck/waste using the de-wateringunit 114 at node 6. Potable water can also be added from an outsidesource as required, such as when the REM apparatus 100 is firstcommissioned. The ECU 118 controls the dilution process based onmeasurements obtained with level sensing equipment.

After the required amount of dilution liquid (e.g., potable and/or greywater) is added to the muck/waste in the mixing tank 202, thehomogenizing pump 204 macerates the water/muck/waste mixture to obtainthe desired viscosity. That process should take only a few minutes aday, after which, there should be a sufficient amount of homogenizedwater/muck/waste to begin pasteurization and digestion. The homogenizingpump 204 is preferably configured to process 0.5 metric tons ofwaste/muck an hour. And as discussed above, the REM apparatus 100 can besized using modular components are required to process user-specificdaily amounts of muck/waste.

At node 2, the water/muck/waste mixture produced at node 1 istransferred into the buffer tank 108 for pre-heating. The buffer tank108 includes a heat exchanger 156 that cools the heated and partiallypasteurized or digested water/muck/waste produced during pasteurizationin the small holding tanks 110 at node 3 while warming thewater/muck/waste mixture produced with at node 1. The heat energy lostby the heated and partially pasteurized or digested water/muck/wasteduring cooling is transferred to the water/muck/waste mixture in thebuffer tank 108 to warm it from its ambient temperature before it ismoved to the small holding tanks 110. That process allows thewater/muck/waste mixture going into the large digester to be at 35-40°C. so as to avoid thermal shock to mesophilic bugs in the large holdingtank 112 at node 4. It also pre-heats the water/muck/waste mixtureproduced at node 1 so that less load is placed on the heaters 160 in thesmall holding tanks 110 at node 3, where the water/muck/waste mixture isheated to at least 70° C.

At node 3, the small holding tanks 110 use a gas mixer 158 to mix thewater/muck/waste mixture with air, which allows bugs to use oxygen toheat up the water/muck/waste mixture during pasteurization. The contentsof those small holding tanks 110 are also warmed with internal heaters160 to an operating temperature of approximately 70° C. for a minimum of60 minutes. That can be adjusted as required to optimize pasteurizationusing a SCADA system connected to the ECU 112 via the SCADA interface.Two or more small holding tanks 110 are preferably provided so that thebugs therein can be quickly and easily cycled through those tanks withfeed, hold, and discharge steps. The feed and discharge steps would bemore time consuming and difficult with larger tanks. Moreover, the loadon the heaters 160 would be greater in larger tanks.

After pasteurization in the small holding tanks 110 is completed, theheated and partially pasteurized or digested water/muck/waste is movedto the large holding tank 112 for mesophilic anaerobic digestions andbiogas recovery at nodes 4 and 5, respectively. As discussed above, thatheated and partially pasteurized or digested water/muck/waste is cooledto 35-40° C. by the heat exchanger 156 in the buffer tank 108 at node 2before it is deposited in the large holding tank 112 until apredetermined fill level is reached. In the large holding tank 112, thepasteurized or cooled and partially digested water/muck/waste iscontinuously stirred with the gas stirrer 158 by re-circulating thebiogas generated during mesophilic anaerobic digestion back into thewater/muck/waste. The feed flowrate to the large holding tank 112 issuch that it provides a minimum retention time of 15 days. Thetemperatures and times at which the water/muck/waste is held in thesmall holding tanks 110 and large holding tank 112 is controlled by theECU 118 so as to operate within the pertinent HACCPs and to comply withlocal, national, and/or international standards, such as U.S. EPAregulation 40 C.F.R. 503.32.

The biogas generated during mesophilic anaerobic digestion at node 4 isremoved from the large holding tank 112 and placed in the gas storagetank 120 at node 5. That biogas is moved to the gas storage tank 120 bythe gas vacuum pump 162 as it is being generated by the mesophilicanaerobic digestion. And after that process is complete, what remains ofthe water/muck/waste mixture is output to the de-watering unit 114 atnode 6. As the large holding tank 112 is being drawn down in thatmanner, biogas is moved from the gas storage tank 120 back into thelarge holding tank 112 so as to maintain an operating pressure of 15-20mbar in the large holding tank 112 during that draw-down process. Then,as the large holding tank 110 is being filled with the next batch ofpasteurized or cooled and partially digested water/muck/waste at node 4,the biogas is moved back into the gas storage tank 120 at node 5.

At node 6, the fully digested water/muck/waste drawn from the largeholding tanks 110 is pumped into the de-watering unit 114 forde-watering. The fully digested water/muck/waste undergoespre-filtration by passing it through fine mesh to aid in the separationprocess. The fully digested water/muck/waste may also undergodesulfurization hydrogen sulphide scrubbing, or sweetening, in thede-watering tank 300. And coagulant may be added to aggregate suspendedsolids in the fully digested water/muck/waste so that they fall to thebottom of the de-watering tank 300, thereby leaving a top layer ofcleaned “grey” water, or liquor, that is re-circulated back into thechopper unit 106 with the mixer feed pump 134B. The bacteria in the greywater can also be used as a feedstock, so it may also be gravity fed tothe liquor tank 126 for storage at node 7.

The solids that fall to the bottom of the de-watering tank 300 form athickened layer of organic fertilizer. The electric motor 304 of thede-watering unit 114 rotates the shaftless screw conveyor disposedwithin the conveyor tube 302 to transport that thickened layer oforganic, solid fertilizer up through the conveyor tube 302 and outthrough the spout 306 disposed at the upper end of the conveyor tube302, where it drops into a bin placed below the spout on the loadingplatform 142. The solid fertilizer, or mulch, collected in that bin ispreferably 75 to 85% dry as a result of that process. And the resultingsolid and liquid fertilizers produced by the digestion process willpreferably be pathogen free.

C. Modular Configurations

Although only two containers 102 and 104 are discussed with respect tothe exemplary embodiments of the apparatus and method disclosed above,the components 106-128 of the REM apparatus 100 can be separated into asmany different containers 102 as are required to suit the particularapplication. For example, a processing container could house the chopperunit 106, the buffer tank 108, the de-watering unit 114, and the ECU118; a digestion container could house the small holding tanks 110, thelarge holding tank 112, and the gas scrubber 114; a CHP container couldhouse the biogas engine 122; a liquor storage container could house oneor more liquor storage tanks 126; and a gas storage container couldhouse one or more gas storage tanks 120. In that configuration, theprocessing container would process all of the muck/waste andwater/muck/waste before and after the anaerobic digestion process; thedigestion container would perform the pasteurization or thermophilicanaerobic digestion, the mesophilic anaerobic digestion, and the biogasscrubbing; and the gas storage container would perform all of the biogasstorage. One or more digestions containers could thereby be added to theprocessing container and gas storage container until the processingcapacity of processing container and/or the storage capacity of the gasstorage container was reached. Accordingly, those containers arepreferably interconnected using standardized piping 136A-136C and wiring138 (e.g., prefabricated piping sections and wiring harnesses) to allowthem to be connected in a modular manner, thereby allowing expansion ofthe REM apparatus 100 to suit substantially any throughout requirement.

By way of more specific example, if the chopper unit 106 in eachprocessing container can process 0.5 metric tons of waste/muck an hour,a user that wants to process 6 metric tons of waste/muck in a 8-hour daycould obtain two processing containers and configure them to operate inunison, thereby allowing that user to process that amount of waste/muckover a 6-hour period. Similarly, two processing containers could beprovided to process 24 metric tons of waste/muck in a 24-hour period.Those two processing containers could then be connected to acorresponding number of digestion containers in a daisy chainconfiguration using the aforementioned standardized piping 136A-136C andwiring 138.

Because the anaerobic digestion process typically requires a ratio ofabout 1:4 of waste/muck to dilution liquid (e.g., potable and/or greywater), processing 6 metric tons of waste/muck a day will produceapproximately 30 tons of water/waste/muck mixture (6 metric tonswaste/mulch+(4×6) metric tons dilution liquid=30 metric tonswater/waste/muck mixture). And, because the digestion process in thelarge holding tanks 110 will take approximately twenty-one days,approximately 630 metric tons (˜630 m³) of storage will be required toallow a continuous cycle of waste/muck to be processed at a rate of 6metric tons per day (30 metric tons/day×21 days/digestion cycle=630metric tons/digestion cycle). Thus, twelve digestion containers, eachhaving four 1,800 Liter small holding tanks and two 14,000 Liter largedigestion tanks 112, would be needed to digest 30 metric tons ofwater/waste/muck mixture in that 21-day period, as illustrated in FIG.8.

That 6-ton per day solution is estimated to create 600 m³ of biogas at55-60 percent methane. In such a large capacity process, two gas storagecontainers would need to be provided to store that biogas and at leasttwo CHP containers would need to be provided to convert that biogas intoheat and/or electricity, as also illustrated in FIG. 8. Preferably, atleast three biogas engines 122 will be provide between those two CHPcontainers so that two biogas engines 122 can be used to burn the biogasand the third can be used as a back-up.

Also in that 6-ton per day configuration, two liquor storage containerswould be needed to store the grey water removed from the fully digestedwater/muck/waste after anaerobic digestion is complete. A mulch storagecontainer may also be provided for storing the solid fertilizergenerated from the fully digested water/muck/waste after the grey wateris removed. Those additional containers are also illustrated in FIG. 8.

Each of the processing containers, digestion containers, CHP containers,liquor storage containers, gas storage containers, and mulch storagecontainers discussed above is preferably a standard 20-foot container.If a larger capacity of processing is required, 40-foot containers mayalso be used. And, if 40-foot containers are not suitable, modularcustom containers can be used to suite the required capacity. Thosecustom containers can be assembled on site from pre-formed insulatedconcrete or metal panels. The custom containers can be erected on aconcrete slab that is poured on site by wiring or bolting the pre-formedpanels together. The custom containers can be squared, can have roundededges, can have a domed roof, or any other suitable configuration.

The large holding tanks 112 can be formed in a substantially similarmanner if required. By way of example, if 24 metric tons of waste/muckis desired to be processed in a day, two processing containers can beprovided with three custom large holding tanks 112 formed as describedabove—two for storing the water/waste/muck mixture during the digestionprocess and one for holding that mixture if/when a problem occurs withone of the other large holding tanks.

By making the processing containers, digestion containers, CHPcontainers, liquor containers, gas storage containers, and mulch storagecontainers of the present invention modular, an REM apparatus 100 can beput together from those containers to suit substantially anyapplication. Thus, instead of having to build a new and different wastetreatment plant for every application, the REM apparatus 100 of thepresent invention can be sized to suit. Moreover, by separating thecomponents 106-114 in the processing containers and the biogas engines122 in the CHP containers from the small holding tanks 110, largeholding tanks 112, and gas storage tanks 120, the potential danger ofaccidentally igniting the biogas generated and/or stored in those tanksis avoided.

D. Summary

In summary, the present invention provides a novel solution to wastedisposal problems while providing a sustainable source of energy. Afterthe present invention is installed, all the user needs to do is load hisor her waste into the apparatus and the system will process the waste toproduce heat, biogas, electricity, and fertilizer. And after only a fewweeks of use, the user will have a continuous supply of electricity. Thepresent invention provides at least the following advantages: 1) itgenerates electricity from horse muck year round; 2) it converts septicwaste into hot water and/or heat; 3) it eliminates the cost of disposal,unsightly muck heaps, and smelly septic systems; and 4) it generatesuseful bi-products, including solid and liquid fertilizers.

The REM apparatus 100 is an automated plant that requires nointervention except daily feeding with muck/waste. The embodiment ofFIGS. 1A-1E is capable of processing 400 kg of muck/waste (e.g.,feedstock) per day, which is digested over 15 days to produce about2,000 Liters of biogas and a pasteurized mulch product that meets orexceeds the PAS 110 quality protocol. The grey water, or liquor, alsomeets or exceeds that quality protocol. The REM apparatus 100 is alsodesigned to process muck/waste at temperatures and times within thepertinent HACCPs and that comply with U.S. EPA regulations (e.g., 40C.F.R. 503.32). As discussed above, the ECU 118 is programmed to controlthose temperatures and times. And proper separation of components106-128 is provided as required to comply with the European Union's ATEXdirective and DSEARs.

The apparatus and method of the present invention are particularlysuited for processing waste/much such as organic and septic waste,including but not limited to various types of farm animal manure (e.g.,horse, cow, pig, and chicken manure); meat, blood, and otherslaughterhouse waste; garden and agricultural green waste; foodpreparation and kitchen waste; wasted/leftover/spoiled food; and septictank contents. That muck/waste is digested with a mix of bacteria in ananaerobic digestion process to produce biogas (e.g., methane and carbondioxide), and what remains of the muck/waste after that process isseparated into a dry mulch and a liquid fertilizer. The biogas can becombusted in a CHP unit to generate heat and electrical power; the mulchcan be used as animal bedding; and the liquid fertilizer can be used toput back into the soil to increase its nutrient content and fertility.Moreover, excess electricity generated with the CHP can be sold back tothe national grid.

The foregoing description and drawings should be considered asillustrative only of the principles of the invention. The invention maybe configured in a variety of shapes and sizes and is not intended to belimited by the preferred embodiment. Numerous applications of theinvention will readily occur to those skilled in the art. For example,the mixers 138 may comprise rotational mechanical stirring devicesrather than air nozzles and the biogas engine 122 may be a biogasgenerator rather than a CHP. Therefore, it is not desired to limit theinvention to the specific examples disclosed or the exact constructionand operation shown and described. Rather, all suitable modificationsand equivalents may be resorted to, falling within the scope of theinvention.

What is claimed is:
 1. A renewable energy microgeneration apparatuscomprising: one or more portable containers comprising: a plurality offirst holding tanks that are configured to perform at least one ofpasteurization and thermophilic anaerobic digestion on waste, a secondholding tank that is larger than each of the plurality of first holdingtanks, that is in fluid communication with the plurality of firstholding tanks, and that is configured to perform mesophilic anaerobicdigestion on the waste after at least one of pasteurization andthermophilic anaerobic digestion is performed on the waste, and ade-watering unit in fluid communication with the large holding tank thatis configured to dry what remains of the waste after mesophilicanaerobic digestion is performed on the waste; and a controller forautomatically moving the waste between the plurality of first holdingtanks, the second holding tank, and the de-watering unit as required tofacilitate mesophilic anaerobic digestion in the second holding tank,wherein the one or more portable containers are configured to betransported to a site and placed in fluid communication with each otherat the site.
 2. The apparatus of claim 1, further comprising: a mixingtank for mixing the waste with a liquid; and a chopper in fluidcommunication with the mixing tank and the plurality of first holdingtanks that is configured to macerate the waste into smaller piecesbefore the macerated waste is moved to one of the plurality of firstholding tanks
 3. The apparatus of claim 2, wherein the mixing tank andchopper are provided in separate containers from the one or moreportable containers that comprise the plurality of first holding tanks,the second holding tank, and the de-watering unit.
 4. The apparatus ofclaim 1, wherein: the controller is configured to move the waste to theplurality of first holding tanks and the second holding tank in a batchmode; and the batch mode comprises: moving a first load of waste to oneof the plurality of first holding tanks while at least one ofpasteurization and thermophilic anaerobic digestion is being performedon a second load of waste in another of the plurality of first holdingtanks; moving the second load of waste from the other of the pluralityof first holding tanks to the second holding tank after at least one ofpasteurization and thermophilic anaerobic digestion is performed on thesecond load of waste; moving a third load of waste to the other of theplurality of first holding tanks while at least one of pasteurizationand thermophilic anaerobic digestion is being performed on the firstload of waste in the one of the plurality of first holding tanks; andmoving the first load of waste from the one of the plurality of firstholding tanks to the second holding tank after at least one ofpasteurization and thermophilic anaerobic digestion is performed on thefirst load of waste.
 5. The apparatus of claim 1, wherein each of theplurality of first holding tanks is configured to perform at least oneof pasteurization and thermophilic anaerobic digestion with at least oneof a heater and bugs.
 6. The apparatus of claim 5, wherein each of theplurality of first holding tanks is configured to perform at least oneof pasteurization and thermophilic anaerobic digestion with both aheater and bugs.
 7. The apparatus of claim 1, wherein each of theplurality of first holding tanks is configured to stir the wastedisposed therein with a gas mixer.
 8. The apparatus of claim 1, whereinthe second holding tank is configured to stir the waste disposed thereinwith a gas mixer.
 9. The apparatus of claim 1, wherein the de-wateringunit is configured to generate solid fertilizer and liquid fertilizerwhile drying what remains of the waste after mesophilic anaerobicdigestion is performed on the waste.
 10. The apparatus of claim 1,wherein each of the plurality of first holding tanks and the secondholding tank each comprise at least one level sensor and at least onetemperature sensor, wherein the controller is configured toautomatically move the waste between the plurality of holding tanks, theholding tank, and the de-watering unit by: moving the waste into one ofthe plurality of first holding tanks until the at least one level sensorin that first holding tank indicates that a predetermined volume ofwaste is disposed in that first holding tank; moving the waste from theone of the plurality of first holding tanks to the second holding tankafter the at least one temperature sensor in that first holding tankindicates that the waste disposed in that first holding tank has beenwithin a predetermined temperature range for a predetermined period oftime; and moving the waste from the large holding tank to thede-watering unit after the at least one temperature sensor in the secondholding tank indicates that the waste disposed in the second holdingtank has been within a predetermined temperature range for apredetermined period of time.
 11. The apparatus of claim 10, wherein thecontroller further is configured to automatically move the waste betweenthe plurality of holding tanks, the holding tank, and the de-wateringunit by stopping the waste from being moved from the one of theplurality of first holding tanks to the second holding tank when the atleast one level sensor in the second holding tank indicates that apredetermined volume of waste is disposed in the second holding tank.12. The apparatus of claim 1, further comprising a gas scrubber in fluidcommunication with the second holding tank that is configured to treatgas generated by mesophilic anaerobic digestion so that the gas may beburned as fuel.
 13. A process for renewable energy microgenerationcomprising the steps of: transporting one or more portable containersand a controller to a site, the one or more portable containerscomprising a plurality of first holding tanks, a second holding tank,and a de-watering unit; performing at least one of pasteurization andthermophilic anaerobic digestion on the waste with the plurality offirst holding tanks; performing mesophilic anaerobic digestion on thewaste with the second holding tank after at least one of pasteurizationand thermophilic anaerobic digestion is performed with the plurality offirst holding tanks, the second holding tank being larger than each ofthe plurality of first holding tanks; drying what remains of the wastewith the de-watering unit after mesophilic anaerobic digestion isperformed on the waste; automating the flow of the waste between theplurality of first holding tanks, the second holding tank, and thede-watering unit with the controller as required to facilitatemesophilic anaerobic digestion in the second holding tank.
 14. Themethod of claim 13, further comprising the steps of: mixing the wastewith a liquid in a mixing tank; and macerating the waste into smallerpieces with a chopper before moving the macerated waste to one of theplurality of first holding tanks.
 15. The method of claim 14, whereinthe mixing tank and chopper are provided in separate containers from theone or more portable containers that comprise the plurality of firstholding tanks, the second holding tank, and the de-watering unit. 16.The method of claim 13, wherein the step of automating the flow of thewaste between the plurality of first holding tanks, the second holdingtank, and the de-watering unit with the controller comprises the stepsof: moving a first load of waste to one of the plurality of firstholding tanks while at least one of pasteurization and thermophilicanaerobic digestion is being performed on a second load of waste inanother of the plurality of first holding tanks; moving the second loadof waste from the other of the plurality of first holding tanks to thesecond holding tank after at least one of pasteurization andthermophilic anaerobic digestion is performed on the second load ofwaste; moving a third load of waste to the other of the plurality offirst holding tanks while at least one of pasteurization andthermophilic anaerobic digestion is being performed on the first load ofwaste in the one of the plurality of first holding tanks; and moving thefirst load of waste from the one of the plurality of first holding tanksto the second holding tank after at least one of pasteurization andthermophilic anaerobic digestion is performed on the first load ofwaste.
 17. The method of claim 13, wherein the step of performing atleast one of pasteurization and thermophilic anaerobic digestion withthe plurality of first holding tanks is performed with at least one of aheater and bugs.
 18. The method of claim 17, wherein the step ofperforming at least one of pasteurization and thermophilic anaerobicdigestion with the plurality of first holding tanks is performed withboth the heater and bugs.
 19. The method of claim 13, further comprisingthe step of stirring the waste disposed in each of the plurality offirst holding tanks with a gas mixer.
 20. The method of claim 13,further comprising the step of stirring the waste disposed in the secondholding tank with a gas mixer.
 21. The method of claim 13, wherein thestep of drying what remains of the waste with the de-watering unitresults in the generation of solid fertilizer and liquid fertilizer. 22.The method of claim 13, wherein: each of the plurality of first holdingtanks and the second holding tank each comprise at least one levelsensor and at least one temperature sensor; and the step of automatingthe flow of the waste between the plurality of holding tanks, theholding tank, and the de-watering unit with the controller comprises thesteps of: moving the waste into one of the plurality of first holdingtanks until the at least one level sensor in that first holding tankindicates that a predetermined volume of waste is disposed in that firstholding tank; moving the waste from the one of the plurality of firstholding tanks to the second holding tank after the at least onetemperature sensor in that first holding tank indicates that the wastedisposed in that first holding tank has been within a predeterminedtemperature range for a predetermined period of time; and moving thewaste from the large holding tank to the de-watering unit after the atleast one temperature sensor in the second holding tank indicates thatthe waste disposed in the second holding tank has been within apredetermined temperature range for a predetermined period of time. 23.The method of claim 22, wherein the step of automating the flow of thewaste between the plurality of holding tanks, the holding tank, and thede-watering unit with the controller further comprise the steps ofstopping the waste from being moved from the one of the plurality offirst holding tanks to the second holding tank when the at least onelevel sensor in the second holding tank indicates that a predeterminedvolume of waste is disposed in the second holding tank.
 24. The methodof claim 13, further comprising the step of treating gas generated bymesophilic anaerobic digestion with a gas scrubber so that the gas maybe burned as fuel.